Hydrophilic-poromeric foam

ABSTRACT

THIS INVENTION IS A HYDROPHILIC AND POROMERIC FOAM MADE BY A UNIQUE PROCESS THAT IS ADAPTED TO BE MADE INTO A SYNTHETIC LEATHER-LIKE MATERIAL HAVING MANY OF THE DESIRABLE AESTHETIC AND PHYSICAL PROPERTIES OF NATURAL LEATHER AND, IN ADDITION, IS MADE FROM RELATIVELY INEXPENSIVE MATERIALS.

United States Patent-015cc 3,778,332 Patented Dec. 11, 1973 3,778,332 HYDROPHILIC-POROMERIC FOAM Eugene B. Butler, Kent, Ivan A. Fak, Munroe Falls, and

Lawrence L. Line, Kent, Ohio, assignors to The General Tire & Rubber Company 1 No Drawing. Original application June 1, 1970, Ser. No. 42,592, now Patent No. 3,644,229. Divided and this application July 28, 1971, Ser. No. 167,018

Int. Cl. B32b 3/26, 5/18 US. Cl. 161-159 3 Claims ABSTRACT OF THE DISCLOSURE This invention is a hydrophilic and poromeric foam made by a unique process that is adapted to be made into a synthetic leather-like material having many of the desirable aesthetic and physical properties of natural leather and, in addition, is made from relatively inexpensive materials.

This is a divison of application Ser. No. 42,592, filed June 1, 1970 and now US. Pat. 3,644,229.

BACKGROUND OF THE INVENTION Field of the invention This invention relates to the field of synthetic poromeric materials sometimes known as man-made leathers. More particularly, this invention relates to synthetic leather materials based on vinyl chloride polymers that are specially fortified with urethane polymers.

DESCRIPTION OF THE PRIOR ART Synthetic poromeric materials find their widest use in articles that are in contact with or adjacent to the human body, such as footwear and furniture upholstery, so that the poromericity enables removal of accumulated moisture from the skin and makes the user more comfortable.

Synthetic poromeric materials also have other properties that make them desirable; scuff resistance of natural leather is rather low resulting in rapid wearing of the finish and surface of leather articles whereas synthetic poromerics exhibit a high degree of scuff resistance and have doubled or tripled the useful life of some articles made therefrom such as shoes. In addition, the scuff resistance of these synthetic poromerics relieves and in many cases eliminates the need for polishing. Other properties such as the ability to hold shape, water repellency, high strength, and high tear resistance have given these man-made materials a firm commercial position.

These materials have not, however, achieved the degree of commercial acceptance originally predicted. There are many theories as to why this is but none have been definitely established. It appears, however, that one of the major reasons for this rather restricted acceptance has been the high cost of the materials along with the inability to combine most or all of the desirable aesthetic and other properties of natural leather.

As an example, most man-made leathers do not equal natural leather in the degree of hydrophilicity even though they surpass natural leather in many cases in the property of poromericity. The disparity between natural and man-made leather in regard to these two properties is striking; for instance, most man-made leathers are of a magnitude of 2 to times more poromeric than natural The term hydrophilicity or hydrophilic is generally defined as the property of having an aifinity for water. The term poromerietty or poromeric has not received such extensive use as to mark its place in common dictionaries, however, it is generally used in the shoe trade to define the property of passing moisture vapor across or through a membrane lghrough the apparent utilization of tiny pores in the memrane.

leather whereas they absorb Water or are hydrophilic only to the extent of about 7 percent of natural leather.

This may be the reason that persons wearing man made leather shoes complain that the shoes are hot wearing, i.e. the foot perspires faster than the poromeric material can transmit the moisture to the outside of the shoe (for evaporation) so that this excess moisture is not otherwise absorbed or removed and therefore puddles or accumulates in the stocking to cause uncomfortableness. It is, of course, well known that shoes made of natural leather absorb (by hydrophilicity) a large amount of moisture from the foot during the time they are worn and give up this moisture (dry out) when not used; this absorption of foot perspiration makes the natural leather shoe noticeably cooler wearing.

The prior art has had extreme difficulties in combining many of the aesthetic and other properties, most importantly poromericity and hydrophilicity, into man-made leather while retaining other properties at desired levels. For instance, it is known to mechanically whip air into (i.e. froth) a polyvinyl chloride plastisol resin containing an emulsifier and then fuse it to form a polymeric hydrophilic foam. (Reference US. Pats. 3,28,920; 3,301,798; and 3,432,449) however, these foams have extremely poor scuff resistance, tensile strength, and tear strength so that they cannot be used as direct replacements for man-made leathers. It is also known that polyvinyl chloride plastisols may be saturated into fibrous mats, chemically blown, and then compressed during fusing to give a rather strong poromeric material (reference U.S. Pat. 2,917,405), however, such a material is not hydrophilic and does not exhibit the aesthetic properties of break, drape, and hand suflicient to be utilized as a replacement for natural leather. Further still, it is known to combine water and a polyester with a vinyl chloride plastisol and thereafter treat it with a polyisocyanate to form a chemically blown, closed cell cushion material of rather high strength (reference US. Pat. 2,898,312); however such material is neither poromeric nor hydrophilic.

This invention is based upon the discovery that a hydrophilic-poromeric foam may be inexpensively made that is strong and highly abrasion resistant and furthermore that may be made into a synthetic leather material incorporating so many of the aesthetic :and other properties of natural leather that only the most discerning individual can tell that it is not a natural leather product. The foam of this invention comprises a cured frothed mixture of a fluidic blend comprising a vinyl plastisol and a specific emulsifier with a limited amount of a fiuidic polyurethane precursor in such a manner as to form a light weight frothed material. This foam and products made therefrom combine the properties of poromericity and hydrophilicity similar to natural leather with exceptional scuff resistance, tensile strength, and certain other properties, mostly in excess of the respective properties of natural leather, while at the same time costing substantially less on a volume basis than most man-made leathers. The foam may be used alone, utilized as a top coating for fabrics and other substrates, used in supported sheets for a variety of purposes, and also saturated into a fibrous mat to form the above-disclosed synthetic leatherlike material.

Therefore, the main object of this invention is a synthetic poromeric-hydrophilic foam for use in a wide range of products and articles. Other objects include a composition that is mechanically frothed to give a uniform cell size and that has exceptional physical and aesthetic properties among them being hydrophilicity upwards of percent by Weight and good hand, break, drape, wetstrength, flexibility, etc.; a process that produces a poromeric-hydrophilic material of uniform cell size in a variety of densities and that is applicable to produce supported and unsupported materials as well as saturants and top coatings, that utilizes a relatively small amount of equipment, and that is amenable to automatic and semiautomatic process control; and a synthetic leather material made by saturating the novel composition into a fibrous material that combines poromericity and hydrophilicity with exceptional scuff resistance, hand, feel, flexibility, tensile strength, elongation, and tear resistance.

SUMMARY OF THE INVENTION This invention concerns a hydrophilic, poromeric foam comprising the cured frothed mixture of (I) a fluidic blend comprising 100 parts by weight of a plastisol grade vinyl chloride resin, between about 50 to 100 parts by weight of at leat one compatible liquid platicizer, a stabilizer for the vinyl chloride resin and about to about 16 parts by weight of an emulsifier comprising between 36-46 weight percent of a saturated or unsaturated fatty acid having from 12-24 carbon atoms or mixtures thereof; between 27-37 weight percent of an alkali salt of a saturated or unsaturated fatty acid having from 12- 24 carbon atoms or mixtures thereof; between 6-16 percent of a member selected from the group consisting of potassium acid phthalate, sodium phthalate, and sodium acid phthalate; between 4-8 weight percent water; between 4-6 weight percent of a saturated aliphatic glycol; between 2-4 weight percent of a low molecular weight hydrocarbon oil; and between 1.5-2.5 weight percent of silicic acid; and, (II) between about 7 to about 19 parts by weight of a fluidic polyurethane precursor prepared from the reaction between a polyol and a polyisocyanate.

DESCRIPTION OF THE PREFERRED EMBODIMENT The poromeric-hydrophilic foam of this invention may be used in a wide variety of products especially where body comfort is of prime concern. There are many articles that may be covered with or employ this material such as furniture and upholstery therefor, clothing, gloves, seats and cushions, beds and the like, and footwear. As will be described in more detail later, the foam may be produced in sheets and films, cast upon a backing material, or saturated into fibrous mats. All such uses are fully contemplated in this invention.

The hydrophilic-poromeric foam of this invention is made from two components, the first of which (1) comprises a plastisol grade vinyl chloride resin, at least one compatible liquid plasticizer therefor, and a special emulsifier to be hereinafter more specifically enumerated.

Vinyl chloride resins are well known polymerized materials made from vinyl chloride monomer. Vinyl chloride is produced by a number of different processes such as by the reaction between hydrogen chloride and acetylene in the presence of a catalyst and by splitting of hydrogen chloride from dichloroethane by hydrochlorination with alkalis. Polyvinyl chloride finds wide use in this invention and may be produced from polymerization of vinyl chloride monomer in a variety of ways such as by bulk polymerization, solution polymerization, and emulsion polymerization.

The primary technique of producing plastisol grade polyvinyl chloride resin is by emulsion polymerization. As is well known in the art, emulsion polymerization involves emulsifying the liquid vinyl chloride monomer in water by the use of surface active agents and agitation and thereafter promoting polymerization through the use of heat, catalysts, or a combination thereof. Emulsion polymerized polyvinyl chloride resin is a fine powder of a particle size suflicient to enable compounding with plasticizers to produce vinyl plastisols.

Plastisol grade polyvinyl chloride resin, as well as other vinyl chloride resins, are characterized mainly by their average molecular we g through the nomenclature of intrinsic viscosity or IV. Generally the intrinsic viscosity or IV of a polyvinyl chloride resin ranges from less than 0.40 to in excess of 2.00. Resins in this whole range of intrinsic viscosities may be used in this invention, however, those in the viscosity range of about 0.60 to about 1.30 are preferred for their case in processing, mixing, frothing, and shaping.

The plastisol grade polyvinyl chloride resin may be extended, diluted, or admixed with up to about 50% by weight with extender resins. Extender resins are generally low cost compatible (usually vinyl) resins whose main function is to reduce overall material cost without adversely affecting chemical or physical properties. This invention contemplates the use of up to 50% extender resins without serious effect on the strength of the final product. Examples of extender resins include polyvinyl chloride-vinyl acetate copolymers, polyvinyl chloridevinylidene chloride copolymers, polyvinyl acetate, polyvinyl alcohol, polyvinylidene chloride, polyvinyl chloridepolybutadiene blends, and the like.

To the plastisol grade polyvinyl chloride resin is added at least one compatible liquid plasticizer. As in the case with almost all vinyl plastisols, the resin particles do not absorb the plasticizer until the later fusing operation so that this mixture of resin and plasticizer remains fluid. Later during curing, the resin particles absorb the plasticizers and form a mass of swollen particles. Upon further heating the resin particles fuse together to form a homogeneous matrix of resinous material wherein the plasticizer is homogeneously distributed throughout to render the cured product soft and pliable and to give the product its properties of drape, flexibility, hand and the like.

A number of plasticizers are available for this purpose and are contemplated in this invention. They range from the simple organic molecular structures, such as dioctyl phthalate, through the more highly branched molecules, such as butyl cyclohexyl phthalate, to the reactive plasticizers containing epoxy or other groups such as epoxidized soybean oil. Examples of other plasticizers usable herein include dibenzyl sebacate; dibutyl phthalate; dibutyl sebacate; dicapryl phthalate; bis-(diethylene glycol monoethyl ether) phthalate; di-(Z-ethylhexyl) acetate; di- (Z-ethylhexyl) phthalate; diisobutyl phthalate; dimethyl phthalate; di-Z-ethylhexyl adipate; dioctyl sebacate; phenol-formaldehyde thermoplastic resins; aromatic hydrocarbons from petroleum; di-iso-octylphthalate; iso-octyliso-decyl phthalate; di-iso-decyl adipate; butyl iso-decyl phthalate; butyl octyl phthalate; dioctyl adipate; normal octyl-normal decyl phthalate; di-iso-decyl phthalate; and the like. The plasticizer and the polyvinyl chloride resin (with or without extender resins) are admixed together under mild agitation to produce a fluidic blend.

To the plastisol grade vinyl chloride resin and compatible liquid plasticizers is added a special emulsifier consisting of between 36-46 weight percent of a saturated or unsaturated fatty acid or mixtures thereof having from 12 to 24 carbon atoms, between 27-37 weight percent of an alkali salt of a saturated or unsaturated fatty acid or mixtures thereof having from 12 to 24 carbon atoms, between 6-16 weight percent of a member selected from the group consisting of potassium acid phthalate, sodium phthalate, and sodium acid phthalate, between 4-8 weight percent water, between 4-6 weight percent of a saturated aliphatic glycol, between 2-4 weight percent of a low molecular weight hydrocarbon oil, and between l.5-2.5 weight percent of silicic acid. An emulsifier of this type is commercially available from the R. T. Vanderbilt Company, Inc., New York, NY. under the trademark FOMADE B. This emulsifier, which is a light brown colored paste, is the only type of emulsifier known that will stabilize a frothed mixture of the plastisol grade vinyl chloride resin compatible liquid plasticizer, and the fluidic polyurethane precursor (to be hereinafter disclosed) throughout the frothing and subsequent process steps of this invention.

There are a variety of materials that may be used as the emulsifier components. For instance, the saturated or unsaturated acid may be lauric, myristic, palmitic, stearic, oleic, linoleic, and linolenic acids with oleic acid preferred; the alkali salts of saturated or unsaturated fatty acids may be the sodium or potassium salts of the above listed fatty acids with potassium oleate preferred; and the saturated aliphatic glycol may be polyethylene glycol, polypropylene glycol, and polybutylene glycol with polyethylene glycol preferred. The alkali salts of the saturated or unsaturated fatty acids may be added directly to the emulsifier or prepared in situ; the in situ preparation is fully within the ambit of one skilled in the chemical artit generally comprises the addition of a soap-forming base such as sodium hydroxide, potassium hydroxide, etc. to the fatty acid.

This special emulsifier has an added unique property in that it causes a high degree of trirnerization to take place between the active NCO groups in the precursor such as when the polyurethane precursor is prepared to have active NCO termination at the ends of the molecules. This trimerization appears to explain, at least in part, the unexpected increase in strength and other properties of the foam and materials made therefrom.

The fluidic polyurethane precursor (II) which forms the second component of the foam composition of this invention is prepared from the reaction between a polyol and a polyisocyanate. The polyol may be a polyester or polyether polyol and the preparation of the precursor may be conducted such as to obtain the precursor with active NCO terminal groups capable of further reaction, masked or blocked NCO terminal groups capable of further reaction when unblocked, or a nonreactive or a fully terminated polyurethane precursor. Each of these types of precursors impart separate advantages to certain products made from this composition and all are fully contemplated herein as will be subsequently explained.

The polyols usable herein as the basis of the precursor may be either a polyether polyol, a polyester polyol, or a mixture of the two. They may be selected from a wide range of molecular weights, however, the presence of the vinyl plastisol in fluidic blend (1) and subsequent processing conditions reduces the practical molecular weight range to between about 500 to about 3000. Lower molecular weight polyols, e.g. below about 500, have relatively more polymer chains per unit weight hence there are more chain ends to react with the isocyanate. These lower molecular Weight polyols, while of relatively low viscosity, form an extremely viscous chain-extended precursor and make mixing and frothing of components (I) and (II) difficult. Higher molecular weight polyols, e.g. above about 3000, are viscous to start with and form even higher viscosity precursors causing the same mixing and frothing problems.

The viscosity of the pre-polymer may be lowered by heating or solvent dilution, however, these techniques are severely limited. Heating cannot be taken over about 200 F. as it would cause immediate gelling of the vinyl plastisol in fluidic blend (1). Only high boiling solvents may be used to dilute the viscous precursor as the exotherm produced from mixing of the two components would boil out low-boiling solvents. Furthermore, high boiling solvents have a deteriorating influence on the frothed foam and their use should be limited to only a few parts or less. It has been found successful to use as a diluent some of the compatible liquid plasticizer from fluidic blend (I) and this technique is fully contemplated in this invention.

The precursor is used in a range of about 7 to about 19 parts by weight per 10 parts of the plastisol grade vinyl chloride resin. Below about 7 parts, the polyurethane does not provide sufficient fortification of the foam or enhancement of other properties for utilization in a manmade leather. In contrast, when used in excess of about 19 parts by weight a large quantity of resinous gel particles are produced in the frothing step which impairs the processing and degrades the quality of the foam.

As stated earlier, the precursor may be prepared to contain no reactive isocyanate end groups, contain masked or blocked isocyanate end groups, or contain fully reactive isocyanate end groups. These preparations are fully within the ambit of one skilled in the chemical art. To prepare an unreactive polyurethane precursor one merely reacts a polyol (either polyether or polyester) with a stoichiometric amount of a polyisocyanate so that all of the labile hydrogens in the polyol are reacted with the NCO groups in the isocyanate. To prepare a polyurethane precursor having instantly reactive residual NCO end groups one merely increases the amount of polyisocyanate. To prepare a masked or blocked isocyanate containing polyurethane precursor one may react the polyiso cyanate with a stoichiometric deficiency of a masking agent, which is generally an easily dissociable polyhydric material such as a phenol, a cresol, an alcohol, etc. and thereafter combine that reaction product with the polyol. The residual or nonreacted NCO groups in the polyisocyanate chain-extend the polyol and further reaction therebetween may be occasioned by heating to raise the temperature sufficient to dissociate the masking agent and render the unblocked NCO groups reactive.

Polyester polyols for use herein are formed from the condensation of at least one polyhydric alcohol and at least one polycarboxylic acid. Examples of suitable polyhydric alcohols include the following: glycerol; pentaerythritol; ethylene glycol; diethylene glycol, polypentaerythritol; mannitol; trimethylolpropane; sorbitol; methyltrimethylolmethane; 1,4,6-octanetriol; butanediol; pentanediol; hexanediol; dodecanediol; octanediol; chloropentanediol; glycerol monoallyl ether; glycerol mono-' ethyl ether; triethylene glycol; 2-ethylhexanediol-1,4; 3,3- thiodipropanol; 4,4-sulfonyldihexanol; cyclohexanediol- 1,4; 1,2,6-hexanetriol; 1,3,5-hexanetriol; polyallyl alcohol; 1,3-bis (Z-hydroxyeth) propane; 5,5-dihydroxydiamyl ether; tetrahydrofuran-Z,S-dipropanol; tetrahydrofuran-Z, S-dipentanol; 2,S-dihydroxytetrahydrofuran; tetrahydrothiophene-2,5-dipropanol; tetrahydropyrrole-Z,S-propanol; 3,4,S-hydroxytetrahydropyran; 2,5-dihydroxy-3,4-dihydro- 1,2. pyran; 4,4 sulfinyldipropanol; 2,2-bis (4-hydroxyphenyl)-propane; 2,2'-bis (4 hydroxyphenyl)-methane, and the like. Examples of polycarboxylic acids for use herein include the following: phthalic acid, isophthalic acid; terephthalic acid; tetrachlorophthalic acid, maleic acid; dodecylmaleic acid; octadecenylmaleic acid, fumaric acid; aconitric acid, itaconic acid, trimellitic acid; tricarballylic acid; 3,3'-thiodipropionic acid; 4,4-sulfonyldehexanoic acid; 3-octenedioic-1,7 acid; 3-methyl-3-decenedioic acid; succinic acid; adipic acid; 1,4-cyclo-hexadiene-1,2- dicarboxylic acid; 3-methyl-2,S-cyclohexadiene-1,2-dicarboxylic acid; 8,12-eicosadienedioic acid; 8-vinyl-10-octadecenedioic acid; and the corresponding acid anhydrides, acid chlorides, and acid esters such as phthalic anhydride, phthaloyl chloride, and the dimethyl ester of phthalic acid. Polyethers are generally made by reacting an alkylene oxide such as propylene oxide with a strong base such as potassium hydroxide.

The acid number of the polyester polyol should be maintained at a very low level i.e., below about 5 and preferably at or below about 1.0. The reason for this is that the carboxylic acid group, forming the acid number, will react with the isocyanate to produce a mixed carboxylic-carbamic anhydride which will either lose carbon dioxide to form an amide which will further react with isocyanate and produce an acylurea which causes branching and gel formation in the precursor reaction if there be one or it will disproportionate into a urea or biuret and an hydride wherein the biuret promotes branching and gel formation and wherein the anhydride is hydrolytically unstable and tends to break down (depolymerize) upon exposure to moisture. To preclude these problems, it is desirable to use polyester polyols having acid numbers below about 1.0.

A wide variety of polyisocyanate compounds may be used in the preparation of the precursor. Examples of some of these include toluene-2,4-diisocyanate, toluene-2,6-diisocyanate, 4,4'-diisocyanato diphenyl methane, 1,S-naphthalenediisocyanate, cumene-2,4-diisocyanate, 4-methoxy-1,3-phenylenediisocyanate, 4-chloro-1,3-phenylenediisocyanate, 4-bromo-1,3-phenylenediisocyanate, 4-ethoxy-1,3-phenylenediisocyanate, 2,4-diisocyanatediphenylether, 5,6-dimethyl-1,3-phenylenediisocyanate, 2,4-dimethyl-1,3-phenylenediisocyanate, 4,4-diisocyanatodiphenylether, benzidienediisocyanate, 4-6-dimethyl-1,3-phenylenediisocyanate, 9,10-anthracenediisocyanate, 4,4'-diisocyanatodibenzyl, 3,3-dimethyl-4,4-diisocyanatodiphenylmethane, 2,6-dimethyl-4,4'-diisocyanatodiphenyl, 2,4diisocyanatostilbene, 3,3-dimethyl-4,4'-diisocyanatodiphenyl, 3,3'-dimethoxy-4,4'-diisocyanatodiphenyl, 1,4-anthracene-diisocyanate, 2,4-fluorenediisocyanate, 1,8-naphthalenediisocyanate, 2,6-diisocyanatobenzfuran, and 2,4,6-toluenetriisocyanate.

It is to be understood that mixtures of two or more of these polyisocyanates may be employed. Aromatic isocyanates are preferred, particularly toluene diisocyanate which produces a material having exceptionally fine break and hand-significantly better than any of the other polyisocyanate compounds.

It has been found that when the polyurethane precursor is prepared so that it contains less than about one percent residual reactive isocyanate groups the foam prepared therefrom exhibits a maximum in physical properties in combination with the desirable characteristics of hand, drape, break, etc. When the foam is saturated into a fiberous substrate, such as in the preparation of a manmade leather as hereafter disclosed, it has been found desirable to prepare the polyurethane precursor to contain approximately 2 to percent and more preferably 6 to 7 percent residual reactive isocyanate groups. It is theorized that these NCO groups react in some manner with the fibers in the substrate thereby attaining a high degree of adhesion therebetween; this higher degree of adhesion imparts better physical properties to the cured product in the form of higher tensile strength, higher resistance to pilling and higher abrasion resistance.

In addition, certain observations lead to the conclusion that the emulsifier included in fiuidic mixture (I) as hereinbefore described causes the non-reacted isocyanate groups of the polyurethane precursor to trimerize into a high strength three-dimensional cross linked structure higher strength than that obtained by mere dimerization of the NCO groups. These observations in part include the noticeable lack of generation of CO during mixing of the isocyanate reactive precursor with the water-containing fluidic blend of the plastisol resin, plasticizer and emulsifier. As is known in the art, dimerization of NCO groups is accompanied by evolution of copious volumes of carbon dioxide whereas the trimerization reaction evolves none.

Fluidic blend (I) and precursor (11) may contain other material such as colorants, stabilizers, anti-oxidants, fillers,

flame extinguishers, fungicides, and the like and all are fully contemplated in this invention. Colorants may be added to give color to the final compound and to mask sub-surface discoloration and other visible irregularities and may be used in amounts ranging from about 1 to about 30 parts by weight. Examples of colorants usable herein include inorganic materials such as black iron oxide, manganese blue, iron oxide brown, chrome oxide green, molybd-ate orange, cadmium red, mercury red, aluminum, mango violet, titanium oxide, cadmium yellow and the like and organic materials such as oil black, phthalocyanine blue lake, Zulu Green standard shade, Oil Orange powder, Alizarine Maroon lake, Plasticone Red Deep, Oil Red S powder, Stan-Tone MBS Aluminum, Benzidine yellow, and the like.

Stabilizers may be added to retard degradation of the resin caused by exposure to heat or light and may be used in amounts ranging from about 1 to about 30 parts by weight. Examples of stabilizers usable herein are lead salts such as basic lead carbonate, tribasic lead sulphate, dibasic lead phosphite, tri-basic lead maleate, normal lead stearate, di-basic lead stearate, di-basic lead phthalate, lead silicate, and lead salicylate; barium-cadmium-zinc combinations such as coprecipitated barium-cadmium and cadmium-zinc soaps of lauric, stearic, hydroxystearie, and other fatty acids, organotin compounds such as di-butyl tin dilaurate, di-butyl tin maleate, di-octyl tin maleate, di-butyl mercaptides, and the like; expoxidized oils such as epoxidized soya bean oil, epoxidized esters of tall oil and soya bean oil; chelating agents such as triphenyl phosphite; and others such as benzophenones, triazo compounds, phenyl salicylate, and sodium organo phosphates.

Anti-oxidants may be added to control polymer degradation through reaction with oxygen and ozone in the air and may be used in quantities ranging from a trace to about 10 parts. Examples include hydroquinone monobenzyl ether; akylated bis-phenol; tri (nonylated phenyl) phosphite; 2,2 dihydroxy-4,4'-dimethoxybenzophenone; and the like.

Fillers may be added to extend the compound and reduce its cost and in some cases to strengthen the material and may be used in amounts ranging from about 1 to about 50 parts by weight. Examples include calcium carbonate, magnesium carbonate, aluminum silicate, aluminum hydroxide, basic aluminum sulfate, ammonium sulfate, Kaolin clay, silicon dioxide, calcium sulfate, muscovite, diatomaceous earth, silica, amorphous silica, extender resins, and the like.

Flame extinguishers may be added to reduce the hazard of flame of the material of this invention. Flame retardants such as antimony oxide, tris (2,3)-dibromopropyl phosphate, tetrabromophthalic anhydride, tetrabromobisphenol, perchloropentacyclodecane (65 percent chlorine), C Cl H and the like may be used in quantities ranging from about 1 to about 20 parts by weight.

Fungicides may be added to resist the growth of fungus and other bacteria in the finished material; this is especially important in footwear. These fungicides may be added in amounts ranging from 0.01 part per million to more than 5 parts by weight depending upon the nature and type of fungicide base, i.e., whether the fungicide is tied to a large molecule such as a plasticizer or whether it is added alone. Examples of fungicides usable herein include arsenated-epoxidized soybean oil, bis (tri-n-butyltin) sulfosalicylate, 3,5,4'-tri-bromo salicylanilide, N-(trichloromethylthia) phthalimide, quaternary ammonium naphthenate, phenyl mercury acetate, copper-8-quinolinolate, and the like.

The process of making the hydrophilic-poromeric foam of this invention is extremely important in that the formation of the ingredients, the mixing of the fluidic blend (I) and precursor (II), and the .frothing of the mixture must be accomplished precisely and within the limits hereinafter specified so that the foam is properly developed in regard to cell size, density, and other properties, and so that the finished material exhibits the desirable properties of high abrasion resistance and strength in combination with hydrophilicity and poromericity.

Specifically, fluidic blend (I) is prepared by adding to 100 parts by weight of a plastisol grade polyvinyl chloride resin about 50 to 100 parts by weight of at least one compatible liquid plasticizer, a stabilizer for the polyvinyl chloride resin, and between about 10 to about 16 parts by weight of the aforedescribed special emulsifier. These components may be added in any manner, however, for convenience the plasticizer is added initially, the polyvinyl chloride resin added next, the stabilizer, emulsifier, and other optional additives are then added and mixed under mild agitation for about minutes to form a low viscosity i.e., 20-100 centipoise liquid. Other ingredients such as the aforementioned colorants, flame retardants, fungicides and the like may be added at appropriate levels and all of these ingredients stirred into the fluidic blend.

Separately, a fluidic polyurethane precursor is prepared by reacting a polyisocyanate with either a polyether or polyester polyol. This is generally accomplished under anhydric and inert atmospheric conditions to prevent undesirable side reactions with the isocyanate. As previously described, depending upon the end use of the foam i.e. as a foam per se or as a saturant, the residual NCO content of the precursor may be varied from near zero to about percent. Thereafter, fluidic blend (I) is mixed with between about 7 to about 19 parts by weight of fluidic polyurethane precursor (=II) under mild agitation and in the absence of air or other reactive gases and at room temperature to form the basic material for the foam. During mixing of the two components there is created a noticeable exotherm along with a slight effervescence which may be the result of a slight amount of dimerization of the reacted NCO group with the water and other labile hydrogen containing compounds, a nominal amount of trimerization of the same ingredients catalyzed by one or more of the components of the emulsifier, the heat of mixing of the components or, more realistically, a combination of all three phenomena. The resultant material is a rather viscous fluidic material. This viscous material is thereafter frothed with air or other nonreactive gas, in conventional frothing equipment into a foam having a density of about 0.5 gram per cubic centimeter to about 1.5 grams per cubic centimeter.

Another method of mixing fluidic blend (I) and precursor (-II) is to bring them in separate lines to the mixing head of the frothing equipment so that they are intimately mixed and frothed simultaneously to produce the foam of the above described density range. Neither procedure appears to be better than the other and they may be interchanged and utilized depending upon the exigencies of the process equipment. The viscosity of the foam is attained and controlled by the speed of the frothing mixer and amount of gas injected into the frothing head.

The frothing gas may be virtually any non-reactive gas that does not impart hazardous or dangerous properties to the final foam; examples of gases usable herein include air, nitrogen, carbon dioxide, helium, and the like.

The frothing of the mixture may be produced in many types of frothing equipment such as a common milk shaker or other similar machines. Of particunlar utilization herein is a machine known as an Oakes mixer which is a water jacketed, high speed, emulsifying-whipping machine commercially available in the industry; this particular machine produces a creamy, smooth foam and is the preferred frothing device.

The foam is th'ereafter shaped for the desired product. For instance, the foam may be cast in a layer on a release paper (silicone treated or Teflon treated release paper) and passed through a curing oven. Alternatively, the foam may be cast in a layer over a fabric or other substrate so as to produce a supported material; examples 10 of fabric usable herein include a woven nylon, cotton jersey, nonwoven rayon, etc.

The foam is thereafter subject to heat or other energy input to obtain a cure of the foam. By curing it is meant that the plastisol, i.e., fluidic blend of polyvinyl chloride resin in the plasticizer, will form into the aforesaid swollen particles filled with plasticizer and thereafter fuse into a homogeneous matrix of plasticized polyvinyl chloride. Curing also includes driving to completion the trimerization and/or other polymerization reactions of the polyurethane. For heat curing, the material may be cured over a wide temperature range such as at 450 F. for 15 minutes. Obviously, a lower temperature will require a somewhat longer curing time whereas a higher temperature will require a shorter curing time. Care should be taken that the curing temperature does not exceed the irreversible degradation temperature of the separate components; this aspect of the process is fully within the ambit of one skilled in the plastics art and is contemplated in this invention.

The foam may also be saturated into a fibrous mat and cured to produce a synthetic leather-like material of such look, feel, and other properties that only the most discerning individual can tell that it is not natural leather. The foam is saturated into the fibrous mat by such means as casting the foam on both surfaces of the mat and passing the mat through pressure rolls to force the foam into the interior of the mat. Other processes include dipping the mat in a bath of foam and thereafter running it through a set of squeeze rolls. The fibrous mat may be made of a number of different fibers such as natural, synthetic, and mixtures thereof. Examples of these include nylon, Dacron, Vycron, acrylic, rayon and cotton. All of these fibrous mats produce an extremely high quality synthetic leather material. This material may then be cured in the same manner as the above-described materials.

The synthetic leather material produced above may be split and skived to produce synthetic leathers of different weights and uses. For example, a three denier, 1% inch, staple nylon fiber mat of 15 ounces per square yard may be heavily needled and pressed to form a dense fibrous mat. Said mat may then be saturated with the foam of this invention, cured at 400 F. for 3 /2 minutes, and then split into 45 mil thick sheets (for mens weight shoes) or 35 mil thick sheets (for womens weight shoes).

This material may thereafter be buffed, embossed, printed, etc. and used as is, top-coated with finishes such as urethane and acrylic coatings to more closely simulated leather, or top-coated with more of the same foam. Typical properties of these materials are: tensile strength (p. s.i.) 1150 (warp) 1850 (fill), tear strength (lb./in.)

310 (warp) 450 (fill); elongation (percentage) 8 (warp) 11 (fill); and MVT 8,000 grams per square meter per 24 hours.

The abrasion resistance of this material is measured via a Ford Scuff tester and a Taber Abrasion tester; however, because these are resilient foam structures instead of solid structures, the standard abrasion test is not applicable. Generally, the test is conducted on a sample of foam by running either or both tests to 1000 cycles (of the abrasion device) and checking the surface for evidence of wear. If no wear is evident then the material is rated acceptable whereas if wear is evident the material is unacceptable. Water pickup is determined by soaking the sample in water for 24 hours and determining the amount of weight increase.

The following examples are given to show one skilled in the art an indication of how to practice the invention and to indicate some of the degrees of freedom of ingredients and processing conditions. Unless otherwise noted, all parts are parts per parts of resin and all percentages are percentages by weight.

11 EXAMPLE 1 Two liquid components (I) and (II) were formulated from the ingredients shown below in Table 1a. Fluidic blend (1) was made by slowly adding the plastisol grade 12 weight) and 35 mils (womens weight) and each slice buffed on one side. Below in Table 1b are listed the dillerent samples prepared in this example and some of the physical properties of each.

TABLE 1b Water Tensile Elon- Tear MVT Taber Gauge pick-up strength gation (lbs./ (gJm. abrasion (mils) (percent) (p.s.i.) (percent) in.) 24 hrs.) 1,000 cycles Foam sheet. 20 75 400 250 100 7, 000 Acctgpta e. Cotton jersey supported foam sheet 35 80 950 50 150 6, 500 Do. Nylon mat saturated with foam (men's weight). 45 1, 270 11 220 8, 600 Do. Nylon mat saturated with foam (women's weigh 35 90 1, 000 13 340 0, 600 Do.

polyvinyl chloride resin to the plasticizers under mild agitation and thereafter adding the other ingredients. 15

other reactive gas, for about 15 minutes or until no further exotherm was observed to obtain a polyurethane that contained approximately 6 percent of the original NCO groups in the unreacted state.

TABLE 1a Fluidic blend I: Parts Geon 121 (Plastisol PVC resin--IV=1.19) 100.0

This example shows the operability of the basic process of this invention to produce the novel poromeric-hydrophilic foam and the novel synthetic leather of this inven- I tion. In addition, this example shows that fluidic blend (I) may contain other ingredients in addition to the plastisol polyvinyl chloride resin, at least one compatible liquid plasticizer, and the emulsifier.

EXAMPLE 2 Two liquid components (I) and (II) were formulated from the ingredients shown below in Table 20: except that the intrinsic viscosity of the plastisol grade polyvinyl chloride resin was varied. The method of making the Plasticizer (dioctyl adipate) 25.0 p g mixing them together, and frothins e m Plasticizer (Nuimenitate) 44 0 tuer was identical to that described in Example 1. Plasticizer (99 percent expoxidized soybean oil with 1 percent 1,10 oxybisphenoxarsine fungicide) 4.0 TABLE Barium-cadmium stabilizer 2.0 Sample A B c Emulsifierz 2 15 Fluidic blend (I):

D I Plastisol grade PVC resin (IV =0.75) 100 41we1ghtpercent01e1c acld; filgggggl gggg 5&8 533;; $3395"- ((329152 wgihgtht percetnt potassium oealtleil 1 t llzlastlciie wiocty pththalateyi ""'ig.'g""igfg' 7 .2

Wei percen po aSSIUm 8.01 p a ae; lgmen lron 0x1 0 row E ulslti eT bl 1 15.0 15.0 15.0 6 Welght Parcel!t Water; Precu r or 1196300 13w? gblyesterureth he 6 5 5 i h percent l th l ly ol; 40 percent unreacted NCOitoluene diisocyanater 15.0 15.0 15.0 (6) 3 weight percent of a low molecular carbon oil; and, ZWelght Percent of 5111610 mild; and, Samples A, B, and C were separately saturated into Pr c r III samples of a three denier, 14 ounces per square yard nee- 1000 polyesteTllfetyane 6 Percent unre dled nylon mat by dipping the mat into the frothed mixacted 101116116 dllsocyanate tures of components (I) and (IT), passing the wetted mat through a set of squeeze rolls drying the mat at 350 F 1 B. F. Goodrich Chemical Company. :QFQMADE 13., R. '1. Vanderbilt Company. for 20 minutes and shttmg the mat to a 11111. sheet TABLE 2b Tensile Tear Elon- MVT Water Taber strength strength gation (g./m. pick-u abrasion Ford scufl Sample (p.s.1.) (p.s.i.) (percent) 24hrs.) (percent 1,000 cycles 1,000 cycles 1,900 485 12 8,100 100 Acceptable-.. Acce table. 1,820 400 9 9,350 -d0..- l o. 1,325 350 20 9,600 -.-do Do.

Components (I) and (II) were blended together at room temperature in a nitrogen purged pot under mild agitation for 15 minutes to produce a viscous fluid. The mixture was then pumped (Moyno pump) into an Oakes mixer under a nitrogen blanket; a nitrogen line was attached to the Oakes mixer head and the pressure set at p.s.i.g. The Oakes mixer was set to r.p.m. and the nitrogen flow rate adjusted to pass 23 cubic centimeters of nitrogen per second to the mixer. After lining out, the Oakes mixer produced a foam having a density of 0.73-0.77 gm./cc. The foam was processed in three ways: part of the foam was cast on silicone treated release paper in a 50 mil thickness, more of the foam was cast in a 50 mil thickness onto a cotton jersey backing cloth; and a third sample of foam was saturated into a three denier, 14 ounces per square yard, heavily needled nylon mat. All three samples were passed through the curing oven and cured at 450 F. for 15 minutes. The satuand bufiing one surface thereof. Table 2a shows the physical properties of these samples.

This example shows that the plastisol grade polyvinyl chloride resin usable in this invention may be chosen from a wide range of intrinsic viscosities.

EXAMPLE 3 rated material was split into gauges of 45 mils (mens 75 ical properties.

TABLE 3a 14 This example shows that the compatible liquid plasticizers for fiuidic blend (I) may be chosen from a wide Samnlo A B h range of molecular weights and types. This example 32 3 L 100 75 50 further shows that different types of isocyanates and isom iggfiflgg yg 'fiigfjj 4,0 M M cyanate composltions may be used in making precursor 50 (II).

igmen. on oxi e rown 0.5 0.5 0.5 Plasticizer (dioctylphthalate) 44.0 44.0 44.0 EXAMPLE 5 Plasticizer (epoxidized soyabean 29. 0 29.0 29.0 P Emulsifier (180006 gallcile r 1 Two liquid components (I) and (II) were prepared recursor p0 yeste uret ane percent unreacted NCO, toluene diisocyanate. 15.0 15.0 15.0 10 from the Ingredients shown below In Table except 1 that the type of polyurethane pre-polymer polyol was Extender S1111 Glmdyear Rubber Cmpmyvaried. The components were made, mixed together, and

TABLE 3b Tensile Tear Elon- MVT Water Taber strength strength gation (g./m. pick-u abrasion Ford scufi Sample (p.s.i.) (lbs/in.) (percent) 24hrs. (percent 1,000 cycles 1,000 cycles 1,900 485 12 8,100 100 Acceptable--- Acceptable. 1,400 405 9 9, 500 95 do D0. 900 320 9 10,000 80 do Do.

This example shows that the plastisol grade polyvinyl chloride resin of this invention may be extended with resins and still form an operabe product.

EXAMPLE 4 Two liquid components (-I) and (II) were prepared from the ingredients shown below in Table 4a except that the type of plasticizer and the type of isocyanate were TABLE 5a varied. The components were made, mixed together, and S l frothed iii a manner identical to that described in Example amp e A B C 1 and the foam saturated into a nylon fibrous mat and Fluidic 1016111111 Geon 121 100 100 100 processed as described 1n Example 2. In Table 4b appear Plasticizer(di0ctylphtha1ate) 44.0 44.0 44.0 Plasticizer (polymeric M.W. 4,500). 25.0 25.0 25. 0 the physlcal propertles' 40 glasticizteg (epoxiddizei soya)bean oil) 4.0 4. 0 igmen iron oxi e rown 0. 5 0. 5 TABLE Cadmium-barium stabilizer---.. 4.0 4.0 4.0 Sample A B c D Emulsifier (see Table 1a) 15.0 15.0 15.0

Precursor II: Fluidic blend 1: 1000 M.W. polyesterurethane 6 percent un- Geon 1 21 100 100 100 100 reacted NCO 80/20:2,4/2,6 toluene diisoi i ii E i 00 6006" $3 it. "40

as cizer po y-merrc Plasticizer (polymeric M.W. 3,500) 20 30 1,000 pmyethemmhane 6 l Cadmium-barium stabilizer 4.0 4.0 4.0 4.0 reacted NCO 80/20i214/2r6 toluene (11150 Emulsifier (see Table 1a) 15. 0 15. 0 15. 0 15. 0 cyanateu- 0 Precursor II: 1,000 M.W./1,000 M.W. polyester/polyether ,95% D 1703515el'ur0110 2.10;I $6 0 15 0 15 0 /50 polyurethane 6 percent unreacted percen unreac e 1,000 MW D My estemethane MDI 2 50 N0 8 toluene dusocyenate 15. 0

1,000 M.W. 6 percent unreaeted NCO 15.0 15.0

1 80 percent 2,4-t0luene diisocynaate, 20 percent 2,6-t0lueue diisocyanate 2 100 percent 4,4-diisocyanato diphenylmethane.

TABLE 4b Tensile Tear Elon- MVT Water Taber strength strength gation (gJmfi/ pick-up abrasion Ford scuff Sample (p.s.i.) (lbs/in.) (percent) 24 hrs. (percent) 1,000 cycles 1,000 cycles A 1, 700-1, 800 550-575 80-90 7,000 110 Acceptable Acceptable.

500-580 70-90 7, 400 90 .--..-d0 D0. 2 390- -90 9,560 .-d0 D0. 440-55 85-105 10,300 -..do Do.

TABLE 51) Tensile Tear Elon- Water MVT Taber strength strength gation pick-up (g./m. l abrasion Ford scufl (p.s.i.) (lbs.lin.) (percent) (percent) 24 hrs.) 1,000 cycles 1,000 cycles 950-1325 160-350 8-20 9,600 Acceptable..-. Acceptable. 1, 320-2, 200 320-520 80-105 100 10, 000 d D0. 915-1,700 235-420 13-18 95 9,600 do D0.

foam saturated into a nylon fibrous mat and processed This example shows that the polyurethane prepolymer may be comprised of polyester polyols, polyether polyols, and mixed polyester polyesteher polyols.

EXAMPLE 6 Two liquid components (I) and (II) were prepared from the ingredients shown below in Table 6a except that the type of polyurethane precursor isocyanate was varied. The components were made, mixed, and frothed in a canner identical to that described in Example 1 and the as described in Example 2. In Table 6b appear the physical properties.

10 essed as described in Example 2.

Below in Table 7b are the physical properties of the samples so produced.

TABLE 7b Tensile Tear Elon- Water MVT Taber strength strength gatlon pick-up (g./n1. l abrasion Ford scuff (p.s.l.) (lbs/in.) (percent) (percent) 24hrs.) 1,000 cycles 1,000 cycles 1,000-1,820 260-450 5-9 100 9,500 Acceptabla.-. Acceptable. 1,050-1, 820 250400 6-9 95 9,350 ..d0 Do.

TABLE This example shows that components (I) and (11) may Samnla A B C be reacted prior to being frothed or may be reacted simultaneously with frothing and that the product produced Fluldlc blend I:

Ge 21 100 100 100 therefrom is of the same physical properties. llzlasticizer Editictyl phti\l&a'lati)5 44.0 44. 0 44. 0 25 E MPLE 8 as icizer p0 ymerie 00 25.0 25.0 25.0 XA glasticiier (epoxidized soyabean oil)- 4. 0 4. 0 4. 0

m l clfdniit'lmnaamn stabilizer 2.3 2,8 2.3 Tw liq id mp s nd w re p par d mg g f (See Table 1B) from ingredients shown below in Table 8a. Blending, mix- Polyesterurethaue 6 percent unreaeted NCO 80/20:2,4l2,6 toluene diisocyanate Polyesteruretliane 6 percent nnrcacted ing, and frothing was accomplished in a manner identical to that in Example 1 except that different frothing gases were used. The foams were thereafter saturated into a NCO 65/35:2,4/2,6 toluene diisocyanate 15. 0 g$g g g pg t g 15 0 nylon mat and processed as descnbed in Example 2. In

' so Yam 0 p any me Table 8b appear the physical properties.

TABLE 61) Tensile Tear Elon- Water MVT Taber strength strength gation pick-up (ta/m3; abrasion Ford scuff (p.s.i.) (lbs/in.) (percent) (percent) 24h1s. 1,000 cycles 1,000 cycles 1,125-2,100 300-475 23-11 105 8,100 Acceptable.... Acceptable. 1,002,025 277-500 11-20 95 9, 000 do Do. 950-1,300 200-350 11-20 100 9,600 ....do Do.

' TABLE 8a This example shows that a wide range of isocyanate Fluidic Blend I: Parts compounds may be used in the preparation of the poly- 191 3 1 (d u hth 1 t as icizer iocy p a a e urethane precursor of this invention. Plasticizer (polymeric M.W. 3 500) n 44.0

EXAMPLE 7 Plasticizer (99 percent epoxy lasticizer-1 percent 1,10 oxybisphenoxarsine) 4.0 Two liquid components (I) and (H) were prepared Barlufl l'cadmlum stilbllllei' from the ingredients shown below in Table 7a. The comg gzi fifi Tab 6 1a) ponents were made, mixed, and frothed in a manner iden- 1000 polyesterurethant percent um tical to that described in Example 1. reacted NCO /20:2,4/2,6 toluene dissocyanate 15.0

TABLE 3b Tensile Tear Elon- Water MV T Taber strength strength gation pick-up (g./m. abrasion Ford scuflf Sample (p.s.i.) (lbs/in.) (percent) (percent) 24l1rs.) 1,000 cycles 1,000 cycles A, air irothed- 1,000-1,820 250-400 5-9 100 9,350 Acceptable..-. Acceptable. n ni t r en 1, 050-1, 300 200-400 5-9 100 9,400 Do.

0 Ofcarbon dioxide 1, 050-1, 340 200-420 5-9 Do.

Irothed.

TABLE 7a EXAMPLE 9 Fhgdlc g f g g Two liquid components (I) and (H) were prepared t I hth 1 t 65 from ingredients shown below in Table 9a. Blending, mixi P e) ing, and frothing was accomplished in a manner identical as clzer 10c y a lpa e) to that described in Example 1. The foam was saturated Plasticizer (99 percent epoxy plasticizer-l percent 1,10 oxybisphenoxarsine) 4. Barium-cadmium stabilizer 2.0 Emulsifier (see Table 1a) 15.0

Precursor II:

1000 M.W. polyesterurethane 6 percent unreacted NCO 80/20:2,4/2,6 toluene diisocyanate 15.0

into needled fibrous mats made of different fibers and processed in a manner identical to that described in Ex- 70 ample 2. In Table 9b appear the physical properties.

1 7 TABLE 9a-Continued Fluidic Blend I: Parts (a) 100 parts by weight of a plastisol grade vinyl Plasticizer (99 percent epoxy plasticizer-1 perchloride resin;

cent 1,10 oxybisphenoxarsive) 4.0 (b) between about 50 to about 100 parts by weight Barium-cadmium stabilizer 2.0 of at least one compatible liqui-d plasticizer;

Emulsifier (see Table 1a) 15.0 (c) a stabilizer for said vinyl chloride resin;

Precursor II: (d) between about 10 to about 16 parts by weight reacted NCO 80/20:2,4/2,6 -1 toluene disoof an emulsifier comprising:

1000 M.W. polyesterurethane 6 percent un- (1) between 36-46 weight percent of a satureacted NCO 80/ 20:2,4/ 2,6 toluene diiso- 10 rated or unsaturated fatty acid having from cyanate 15.0 12-24 carbon atoms and mixtures thereof;

TABLE 9b Tensile Tear Taber Elon- Water MVT strength Food scuff strength abrasion gation pick-up (g./m. Material (p.s.i.) 1,000 cycles (lb./in.) 1,000 cycles (percent) (percent) 24 hrs.)

70% nylon, 308% rayon. 850-1, 400 Acceptable-.. 260-375 Acce table 45-75 110 9,700 100% Dacron 830-1, 0 do 260-370 d% 40410 105 100% v crcn 300-375 do 70-100 110 10,000 100% acrylic. 70-110 .-..do 45-85 100 10, 400 100% rayon- 150-180 d0 40-80 95 9,600

(I) a fluidic blend comprising:

Norm-This example shows that the team of this invention may saturated into a wide variety of fibrous mats to produce a high strength, poromeric-hydrophilic material.

EXAMPLE 10 A fluidic mixture was prepared from the ingredients shown below in Table 10. The vinyl chloride resin and the plasticizer were blended together under mild agitation and then the water, polyester resin, and vinyl stabilizer added and blended. To this blend was added 5 parts of an 80/20 mixture of 2,4/2,6 isomers of toluene diisocyanate. Upon addition of the isocyanate, the mixture began to violently foam from the chemical reaction of the isocyanate with the water. Attempts were made to froth this mixture in an Oakes mixer with nitrogen however the mixer jammed with gel so rapidly that no foam could be made.

This example shows that mere addition of a polyol, water, and an isocyanate to a vinyl plastisol does not produce the poromeric-hydrophilic foam of this invention.

(2) between 27-37 weight percent of an alkali salt of a saturated or unsaturated fatty acid having from 12-24 carbon atoms and mixtures thereof;

(3) between 6-16 percent of a member selected from the group consisting of potassium acid phthalate, sodium phthalate, and sodium acid phthalate;

(4) between 4-8 weight percent water;

(5) between 4-6 weight percent of a saturated aliphatic glycol;

(6) between 2-4 weight percent of a low molecular weight hydrocarbon oil; and

(7) between 1.5-2.5 weight percent of silicic acid; and,

(II) between about 7 to about 19 parts by weight of a fluidic polyurethane precursor prepared from the reaction between a polyol and a polyisocyanate.

2. The hydrophilic-poromeric synthetic leather of claim 1 wherein said nonwoven fibrous mat is a nonwoven nylon mat having a weight of about 14 ounces per square yard, wherein the nylon fibers are about 3 denier, and wherein said mat is heavily needled and pressed to a gauge of about 110 mils prior to saturating with said frothed mixture.

3. The hydrophilic-poromeric synthetic leather of claim 1 wherein said emulsifier consists of:

1) 41 weight percent oleic acid; EXAMPLE 11 (2) 32 weight percent potassium oleate; A mixture was prepared of 100 parts of a plastisol (3) 11 weight percent potassium acid phthalate; grade polyvinyl chloride resin, 70 parts of a compatible (4) 6 Weight percent water; liquid plasticizer, 4 parts of a barium-cadmium stabilizer, (5) 5 weight percent polyethylene glycol; and 15 parts of potassium-oleate. This blended mixture (6) 3 weight percent of a low molecular carbon oil; was passed to an Oakes mixer and foamed with air to a and, density of 1.1 grams per cubic centimeter. Thereafter, (7) 2 weight percent of silicic acid.

TABLE 11 0 -u S 0 0 Material Ford seufl Taber abrasion (p rcent g 151). (peg ed?) llisf llin) 2511 3.)

Foam saturated mat 1 o00cyc1esunacceptable-.-- 1,000 cycles unacceptableur- 100 850 45 75 3,500 Foar 1 17cycles ,-table 25 cycles unacceptable 85 200 10 8,500

Norm-This example shows that a polyvinyl chloride plastisol foam saturant does not possess the properties of the team of this invention. one portion of the foam was saturated into a nylon mat Ref r n s Cited and processed in a manner identical to that described in Example 2 and the other portion of the foam was cast UNITED STATES PATENTS on release paper and cured. In Table H above appears the 3,536,638 10/ 1970 Dosmann 161-D1g. 2 physical properties. 7 3,537,947 11/ 1970 Brazdzionis 161--'Dig. 2 The embodiments of the invention in which an exclu- 0 2,801,949 8/1957 Baltemann 151.431 2 sive property or privilege is claimed are defined as follows:

1. A hydrophilic-poromeric synthetic leather comprising a nonwoven fibrous mat saturated with a cured frothed mixture of 3 3 1 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,778,332 Dated December ll 1973 mamas) Eugene B. Butler; Ivan A. Fak and Lawrence L. Line It is certified that error appears inthe above-identified patent and that said Letters Patent are hereby corrected as shown below:

{- Column 2, line 23, which reads: "3,28, 920" should read 1 -'"'3,288:92O"""" Column 6, line' ll, which reads: "(Z-hydroxyeth)" should read ----(2-hydroxyethoxy)---.

Column 7, line .75, which reads: "material" should read ----materials-- 7 Column 10, line 12, which reads: "M50 should read 5o F.---.

Column 12, Table 2a, line HO, which reads: "jtoluene diisocyanater" should read ---toluenediisocyanate---.

Column 13, Table 3a, line 10, which reads: polyesterurethane percent" should read Polyes-terurethane 6 percent--.--. 7

Column 13, line 29, which reads: "operabe" should read ---operable--- 7 Column 13, Table he, line 53, which reads: "2,4-toluene diisocynaate" should read ---2, l-toluene diisocyanate--- Column 15, line 10, which. reads: "canner" should read ----manner---.

Column 15, after line 10, add ---foam saturated into a nylon fibrous mat and processed--- Column 15, Table 6a, line 33, after "unreacted" add ---NCO---.

p040; UNITED STATES. PATENT OFFICE CERTIFICATE OF CORRECTION .Patent: No 3, 78332 Dated December 11, 1,973

Inventor) Eugene B. Butler; Ivan A. Fek and Lawrence L; Line It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:

Column 15 Table 6b, line M0, Sample B, under column 7 entitled Tensile Strength" which reads "l,0 9-- 2,-O2"5'v should read -'-.-v-- -'l',O lO-2,025---. 4 Y

Column 16, TebleBa, line 52, which reads: "polyesterurethantfi should read ---Polyesterurethane---.

' Column l6,v Table 8a, lines 53 a 5 h ch reads; I o y, "dissocyama te"- should read ---diisocyenate'-'-,-s. v 1 I Column 17, Table 9a, deleteline 8 which reads: ."reected,

NCO ,6 -l toluene diso- I e I I n Column Table 9 line 1, which reads: ""InaSr seturated" should read e -may be saturated---. I I I Columns 17 ana 18, Table 11', 1m 59, 6b an 61.; co1umn 5 which reads: "Tensile stength (p .s.i. )"should read ---Tensile strength (p.s.i. i f i Signed ajnd sealed thislBth day of August 197b (SEAL) Att'est:

MCCOY M. GIBSON, JR. I I c'. MARSHALL DANN v Attesting Officer Commissioner of Patents 

